Attachment_2_-_WSWPP_Process_Description.pdf

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BEP ECF Wastewater Pretreatment Plant Maintenance Services
Solicitation number
BEP-RFP-15-0371
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Attachment 2-WSWPP Process

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File Type Posted
Attachment_F-_Questions_and_Answers_Solicitation_BEP-RFP-15-0371.pdf PDF
QASP-Attachment_B-DCF_Wastewater_revised_8-19-15.pdf PDF
BEP-RFP-15-0371-A0005_US.pdf PDF
PWS-BEP_WWPP_Performance_Work_Statement_FFP_Chemical_Update_8-21-15.pdf PDF
BEP-RFP-15-0371-A0004.pdf PDF
Attachment_E_Question_and_Answer_8-12-15_Solicitation_BEP-RFP-15-0371.pdf PDF
BEP-RFP-15-0371-A0003.pdf PDF
Sign-In_Sheet-ECF_Wastewater_Pretreatment_Maintenance_Site_Visit_8-12-15.pdf PDF
BEP-RFP-15-0371-A0002.pdf PDF
QASP-Attachment_B-DCF_Wastewater_revised_7-30-15.pdf PDF
PWS-BEP_WWPP_Performance_Work_Statement.pdf PDF
QASP-Attachment_B-DCF_Wastewater_revised_7-27-15.pdf PDF
BEP-RFP-15-0371-A0001.pdf PDF
Sign-In_Sheet-ECF_Wastewater_Pretreatment_Maintenance_Site_Visits.pdf PDF
BEP-RFP-15-0371_Conform_Copy_7-30-15.pdf PDF
Questions_ _Answers_-__Wastewater_Pretreatment_Plant_Maintenance_Services.pdf PDF
PAST_PERFORMANCE_QUESTIONNAIRE.pdf PDF
Attachment_21_-_Pallets_Specification.pdf PDF
Attachment_18_-_Sodium_Hydroxide_Specification.pdf PDF
Attachment_3_-_PWPP_Process_Description.pdf PDF
Attachment_4_-_GTWPP_Process_Description.pdf PDF
Attachment_8_-_EHS_Contractor_Requirements.pdf PDF
Attachment_10_-_PWPP_Equipment_List.pdf PDF
Attachment_23_-_Spare_Parts_and_Supplies.pdf PDF
BEP-RFP-15-0371.pdf PDF
Attachment_19__-_Sodium-Sulfated_Castor_Oil_Specification.pdf PDF
Attachment_1_-_WW_Permit_017-9.pdf PDF
Attachment_5_-_New_WSR_-_MU_Process_Description.pdf PDF
Attachment_22_-_Process_and_Treatment_Chemicals.pdf PDF
Attachment_6_-_New_WSWPP_Process_Description.pdf PDF
Attachment_26_-_Outfall_Flow_Masurements.pdf PDF
Attachment_B-QASP.pdf PDF
Attachment_27_-_Corrosion_Monitoring.pdf PDF
Attachment_24_-_Nonreimburseable_Tools_-_Janitorial_-_PPE_Supplies.pdf PDF
Attachment_9_-_WSWPP_Equipment_List.pdf PDF
Attachment_13_-_Restricted_Materials_at_DCF.pdf PDF
Attachment_C_Non_Disclosure_Agreement.pdf PDF
Attachment_12_-__EHS_Requirements_for_Purchased_Materials.pdf PDF
Attachment_17_-_Filter_Aid_Specification.pdf PDF
Attachment_15_-_Sulfuric_Acid_Specification.pdf PDF
Attachment_16_-_Sodium_Bisulfite_Specification.pdf PDF
Attachment_7_-_BEP_Furnished_Equipment.pdf PDF
Attachment_11-SCA_Wage_Determination.pdf PDF
Attachment_A_-_Subcontracting_Plan.pdf PDF
Attachment_20_-_Boxes_-_Lids_Specification.pdf PDF
Attachment_25_-_Laboratory_Analysis.pdf PDF
Attachment_14_-_Bentonite_Specification.pdf PDF
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Attachment 2 Wastewater Pretreatment Plant (WWPP) Chemical Treatment Process

Wiping Solution Wastewater Pretreatment Plant (WSWPP)

PROCESS DESCRIPTION: The Wiping Solution Wastewater Pretreatment Plant (WSWPP) is designed to remove the ink solids, minor amounts of oil and grease in the Bureau’s process wastewater discharge, and control the pH limits. The influent to the WSWPP consists of a waste stream that is composed of approximately (1.0%) aqueous sodium hydroxide, emulsified printing inks, approximately (0.5%) castor oil, small quantities of solvents added during press cleaning operations, hydraulic oils from press leaks, and other similar materials. In the WSWPP the wastewater is either pumped or drained from the presses into tank T-1 which serves as a surge tank. The wastewater and ink sludge is then pumped into tank T-3. Bentonite slurry is added to the waste stream prior to the pump so that it can be mixed in line by the pump. The bentonite slurry is added to the waste stream to prevent the sludge from being “tacky” after the acid is added. When too much Bentonite is added, the result is soft filter cakes. When too little Bentonite slurry is added, the ink precipitates and becomes non-pumpable. In tank T-3, sulfuric acid is used to adjust the pH from approximately 12 to 8.5 and Photafloc 3350L is added for coagulation. In the next tank T-4, the pH is finely adjusted from 8.5 to the final of 8.0. Tanks T-5 and T-6 are used as spare process tanks and are connected to T-4 and T-7. In the next tank T-7, a flocculating polymer is added. The wastewater then flows to one of the two gravity settling units (GSU) or (clarifiers). The supernatant water from the GSU then flows to tank T-8 and T-9 and is then pumped through 25µm bag filters to polish the effluent before it is discharged to the sanitary sewer. The sludge is pumped from the GSU to a sludge storage and dewatering tank T-10. The sludge in T-10 is pumped to sludge filter presses where the sludge is concentrated into sludge cakes for disposal. The water discharged from the presses flows to tank T-17 (below grade) and is then pumped back to T-7 for treatment. Spills from the system are collected by the floor sumps and returned to the system for pre-treatment. For any major spill within the plant, a truck well is designed to collect and contain the spill.

T-11 was added to collect wastewater from the press bases which contain substantial amounts of oil/water and collect wastewater from the Wiping Solution Production Plant (WSPP). T-11 acts as an oil/water separator. The wastewater exits T-11, leaving the oil in the tank, and enters the equalization tank T-1. The oil is periodically pumped out of T-11. The wastes are disposed of in accordance with EPA regulations.

PROCESS OPERATION: The Contractor shall operate the WSWPP with prudent engineering and operating practices. Operating the WSWPP includes, but is not limited to, the following tasks:

(1) The Contractor shall take readings every two (2) hours of the pumps data, flows, tank levels, data set points and operating conditions from the computer, and other set points throughout the WSWPP. It should be noted that in the future this may be at least partially performed by SCADA software.

(2) The Contractor shall perform an inspection of the WSWPP every two (2)

Page 2 of 3 Pages hours minimally or more often as needed for proper operation.

(3) The Contractor shall perform a jar test every two (2) hours with samples of

T-7 and T-10 to determine if the sludge is "tacky" and to determine the settling rate and set points (operating parameters) of the WSWPP.

(4) The Contractor shall start, stop, empty filter presses, prepare the pallets, boxes, liners, fill each box to between >2,300 pounds and ≤ 2,400 pounds, band, properly label, and enter the data into the computer logging system which is furnished by the BEP, for the performance of this contract.

(5) The Contractor shall change/clean filter press filter cloths as needed when they become blinded or physically damaged.

(6) The Contractor shall mix the system materials as needed for the optimal operation of the system.

(7) The Contractor shall check pH set points, loop set points, and local set points; and calibrate pH meters weekly at a minimum or more often, as needed.

(8) The Contractor shall respond to all alarms, correcting the conditions to assure proper operation of the WSWPP.

(9) The Contractor shall clean and inspect the tanks at least annually as well as clean the tanks if there is a blockage (build-up) of sludge in any tank as necessary during the operation of the WSWPP.

(10) The Contractor shall order the materials/supplies as needed to assure continuous operation of the WSWPP.

Page 3 of 3 Pages

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